OIL REFINERY
‘Degumming Process’

By :
Izyan Hanis Bt Ramlan
Nor Adilah Bt Sazali
Mursyidah Bt Abdul Gani
Liyana Bt Jamil
Refining of crude oil
•

Crude oils as received from the extraction plant contain several
non-triglyceride components which must be removed.

•

Refining consists of several processes which accomplish this aim.

•

A refining process is carried out following extraction of crude edible oils by means of
screw presses and/or solvent extraction.

•

In refining, physical and chemical processes are combined to remove undesirable
natural as well as environmental-related components from the crude oil.

•

These components comprise for example phosphatides, free fatty acids, pigments
(such as chlorophyll), odors and flavors (including aliphatic aldehyde and ketone),
waxes as well as heavy metals, pesticides etc.
Oil Refining Objectives
1. Removal of undesired products from crude oils
•free fatty acids (FFA)
•phospholipids (gums)
•oxidised products
•metal ions
•colour pigments
•other impurities
2.Preservation of valuable vitamínes.
(vitamina E ortocopherol–natural anti-oxidants)
3.Minimize oil losses
4.Protection of the oil against degradation
1) Degumming for
removal of phosphatides

OIL
REFINING
PROCESS

2)Neutralization for
removal of free fatty acids

3)Bleaching for removal of
color

4) deodorization to distill odors and
flavors
Basic Principle of Degumming
Degumming Process
 Degumming is the first stage in the refining process. It
is sued to separate the gums, phospholipids, proteins
etc… that are insoluble in oil when hydrated.
The aim of degumming operation;
• The emulsifying action of phospholipids increases oil
losses during alkali refining.
• Gums lead brown discoloration of oil after heating
during deodorization.
• Salts may be formed with cooper, magnesium,calcium
and iron, accelerating oxidative degredation of oil.
• Certain phospholipids, such as lecithin, find widespread
industrial application.
Types of Gums Need to Removed :
Two main types
 Hydratable Phosphatides-easy to remove
Non-Hydratable Phosphatides(NHP) -hard to
remove from oil
•some NHP removed with hydratables in
water degumming
•requires the use of a acid to convert to
hydratable for complete removal
1) Water
Degumming

Type of
Degumming
Processes
2) Acid
Degumming

3) Enzymatic
Degumming
Water Degumming
• A large part of the phosphatides (gums) can be hydrated quickly
and easily. If the pressed or extracted oil contains a considerable
quantity of gums the oil is subjected to the water degumming
process immediately following extraction.
• In this process, water is added to the oil. After a certain reaction
period the hydrated phosphatides can be separated either by
decantation (settling) or continuously by means of centrifuges.

• They(Phosphatides) are formed when the oil absorbs water that
causes some of the phosphatides to become hydrated and thereby
oil-insoluble.
• In this process step a large part of hydratable and even a small
proportion of the non-hydratable phophatides are removed. The
extracted gums can be processed into lecithin for food, feed or for
technical purposes.
Steps in Water Degumming
• Heat oil to 60 -70 °C
• Water addition and mixing
• Hydration mixing 30 minutes
• Centrifugal separation of hydrated gums
• Vacuum drying of degummed oil
• Gums -dried for edible lecithin or recombined in meal
Acid Degumming
1) Dry acid degumming: Dry acid degumming is particularly suitable for processing oils with low gum contents such as palm
oil, coconut oil, palm kernel oil or animal fats. Intensive mixing
is implemented following addition of acid to the pre-heated
crude oil. The conditioned gums are absorbed into the
bleaching earth and are separated by filtration.
The benefits of the dry acid degumming process are:
• Efficiency as a result of
– low energy consumption,
– low operation and maintenance costs (sturdy and reliable control
system),

• long service life (the components are acid proof),
• low investment costs,
• environmental-friendly as no wastewater or soap stock occur.
2) Wet acid degumming :Initially oils with higher gum
contents (e.g. corn oil) are similarly processed as in
dry acid degumming. However, to achieve gum
hydration water is added following acid apportioning.
The gums are removed by a separator prior to
bleaching. This process is beneficial as
• centrifuges enable easy separation of gums in oil
types with higher non-hydratable gums contents
(e.g. rape oil and soybean oil),
• the consumption of bleaching earth is reduced
because the oil has already been extensively
degummed.
Dry or wet acid degumming are not always sufficient to
reduce gums to the value required in the oil prior to the
combined deodorization and distillation process.
Thus, a special degumming process is developed.
Steps in Acid Degumming
• Heat oil to 60 -70 °C
• Acid addition and mixing
• Hydration mixing 30 minutes
• Centrifugal separation of hydrated gums
• Vacuum drying of degummedoil
• Gums -recombined in meal
Enzymatic Degumming
Enzymatic degumming was first introduced by the German Lurgi
Company as the »Enzy Max process« .The EnzyMax process can
be divided into four different steps:
1. the adjustment of the optimal conditions for the enzyme
reaction, i.e. optimal pH with a citrate buffer and the
optimal temperature;
2. the addition of the enzyme solution;
3. the enzyme reaction;
4. the separation of lysophosphatide from the oil at
about 75 °C.
Enzymes for enzymatic degumming;
• Lecitase® 10L (pancreatic phospholipase A2)
• Lecitase® Novo (microbial lipase)
• Lecitase® Ultra (microbial lipase)
Steps in Enzymatic Degumming
• The enzyme solution (Aqueous solution of citric
acid, caustic soda and enzymes) is dispersed into
filtered oil at mild temperature,
• a high speed rotating mixer used for effective mixing of
enzyme and oil.
• The conversion of non-hydratable phospholipids
(NHPs) into hydratable phospholipase (HPs) is attained
by the effect of enzyme, t
• the enzyme treated oil is sent to mechanical separation
• the degummed oil received is dried under vacuum and
suitable for further process.
Enzymatic Degumming

Oil refinery(degumming process)

  • 1.
    OIL REFINERY ‘Degumming Process’ By: Izyan Hanis Bt Ramlan Nor Adilah Bt Sazali Mursyidah Bt Abdul Gani Liyana Bt Jamil
  • 2.
    Refining of crudeoil • Crude oils as received from the extraction plant contain several non-triglyceride components which must be removed. • Refining consists of several processes which accomplish this aim. • A refining process is carried out following extraction of crude edible oils by means of screw presses and/or solvent extraction. • In refining, physical and chemical processes are combined to remove undesirable natural as well as environmental-related components from the crude oil. • These components comprise for example phosphatides, free fatty acids, pigments (such as chlorophyll), odors and flavors (including aliphatic aldehyde and ketone), waxes as well as heavy metals, pesticides etc.
  • 3.
    Oil Refining Objectives 1.Removal of undesired products from crude oils •free fatty acids (FFA) •phospholipids (gums) •oxidised products •metal ions •colour pigments •other impurities 2.Preservation of valuable vitamínes. (vitamina E ortocopherol–natural anti-oxidants) 3.Minimize oil losses 4.Protection of the oil against degradation
  • 4.
    1) Degumming for removalof phosphatides OIL REFINING PROCESS 2)Neutralization for removal of free fatty acids 3)Bleaching for removal of color 4) deodorization to distill odors and flavors
  • 5.
  • 6.
    Degumming Process  Degummingis the first stage in the refining process. It is sued to separate the gums, phospholipids, proteins etc… that are insoluble in oil when hydrated. The aim of degumming operation; • The emulsifying action of phospholipids increases oil losses during alkali refining. • Gums lead brown discoloration of oil after heating during deodorization. • Salts may be formed with cooper, magnesium,calcium and iron, accelerating oxidative degredation of oil. • Certain phospholipids, such as lecithin, find widespread industrial application.
  • 7.
    Types of GumsNeed to Removed : Two main types  Hydratable Phosphatides-easy to remove Non-Hydratable Phosphatides(NHP) -hard to remove from oil •some NHP removed with hydratables in water degumming •requires the use of a acid to convert to hydratable for complete removal
  • 8.
    1) Water Degumming Type of Degumming Processes 2)Acid Degumming 3) Enzymatic Degumming
  • 9.
    Water Degumming • Alarge part of the phosphatides (gums) can be hydrated quickly and easily. If the pressed or extracted oil contains a considerable quantity of gums the oil is subjected to the water degumming process immediately following extraction. • In this process, water is added to the oil. After a certain reaction period the hydrated phosphatides can be separated either by decantation (settling) or continuously by means of centrifuges. • They(Phosphatides) are formed when the oil absorbs water that causes some of the phosphatides to become hydrated and thereby oil-insoluble. • In this process step a large part of hydratable and even a small proportion of the non-hydratable phophatides are removed. The extracted gums can be processed into lecithin for food, feed or for technical purposes.
  • 10.
    Steps in WaterDegumming • Heat oil to 60 -70 °C • Water addition and mixing • Hydration mixing 30 minutes • Centrifugal separation of hydrated gums • Vacuum drying of degummed oil • Gums -dried for edible lecithin or recombined in meal
  • 11.
    Acid Degumming 1) Dryacid degumming: Dry acid degumming is particularly suitable for processing oils with low gum contents such as palm oil, coconut oil, palm kernel oil or animal fats. Intensive mixing is implemented following addition of acid to the pre-heated crude oil. The conditioned gums are absorbed into the bleaching earth and are separated by filtration. The benefits of the dry acid degumming process are: • Efficiency as a result of – low energy consumption, – low operation and maintenance costs (sturdy and reliable control system), • long service life (the components are acid proof), • low investment costs, • environmental-friendly as no wastewater or soap stock occur.
  • 12.
    2) Wet aciddegumming :Initially oils with higher gum contents (e.g. corn oil) are similarly processed as in dry acid degumming. However, to achieve gum hydration water is added following acid apportioning. The gums are removed by a separator prior to bleaching. This process is beneficial as • centrifuges enable easy separation of gums in oil types with higher non-hydratable gums contents (e.g. rape oil and soybean oil), • the consumption of bleaching earth is reduced because the oil has already been extensively degummed. Dry or wet acid degumming are not always sufficient to reduce gums to the value required in the oil prior to the combined deodorization and distillation process. Thus, a special degumming process is developed.
  • 13.
    Steps in AcidDegumming • Heat oil to 60 -70 °C • Acid addition and mixing • Hydration mixing 30 minutes • Centrifugal separation of hydrated gums • Vacuum drying of degummedoil • Gums -recombined in meal
  • 14.
    Enzymatic Degumming Enzymatic degummingwas first introduced by the German Lurgi Company as the »Enzy Max process« .The EnzyMax process can be divided into four different steps: 1. the adjustment of the optimal conditions for the enzyme reaction, i.e. optimal pH with a citrate buffer and the optimal temperature; 2. the addition of the enzyme solution; 3. the enzyme reaction; 4. the separation of lysophosphatide from the oil at about 75 °C. Enzymes for enzymatic degumming; • Lecitase® 10L (pancreatic phospholipase A2) • Lecitase® Novo (microbial lipase) • Lecitase® Ultra (microbial lipase)
  • 15.
    Steps in EnzymaticDegumming • The enzyme solution (Aqueous solution of citric acid, caustic soda and enzymes) is dispersed into filtered oil at mild temperature, • a high speed rotating mixer used for effective mixing of enzyme and oil. • The conversion of non-hydratable phospholipids (NHPs) into hydratable phospholipase (HPs) is attained by the effect of enzyme, t • the enzyme treated oil is sent to mechanical separation • the degummed oil received is dried under vacuum and suitable for further process.
  • 16.